Moving bed heat storage and recovery system

ABSTRACT

An energy storage and recovery system designed for storing excess over demand energy generated by a steam cycle electrical generating plant during slack electricity demand periods and for recovering the stored energy to provide supplemental electricity during peak demand periods. 
     The system utilizes one or more moving bed heat exchangers for transferring heat between the steam cycle of the power plant and a moving bed of refractory particles. Pipes and valves establish fluid communication between the heat exchangers and the steam cycle to supply fluid to selectively heat the moving bed of refractory particles or to cool them as the case may be. 
     One or more insulated silos are provided for storing the refractory particles and means are provided for transporting the particles between the silos and the heat exchangers.

This application is a division of application Ser. No. 06/089,824, filedOct. 31, 1979, now U.S. Pat. No. 4,361,009.

BACKGROUND

The present invention relates to energy storage and in particular to athermal energy storage system utilizing moving bed heat exchangers.

Electricity produced by an electric power generating plant must beconsumed immediately or it is lost. The demand for electricity from sucha plant is not constant but varies throughout the day. Thereforeelectric power generating plants must be designed to operate over arange of production levels and moreover, to be capable of producingenough electricity to satisfy peak demands.

Designing the plant to peak load capacity is inherently uneconomical inthat plant construction costs are proportional to capacity. Ideally theplant could be constructed at average load level capcity therebyavoiding the higher construction costs for peak capacity. In order to dothis, peak demands must be met by some supplemental source. Presentavailable sources of supplemental energy for use during peak demandperiods include diesel engines, additional fossil fired steamturbine-generators, and stored energy.

The present invention is an energy storage system designed to supplypeak demand energy for an electric generating facility. According to theinvention, the electric generating plant operates at a constant averageload fuel consumption rate. During slack demand periods, whenelectricity is consumed at less than the average rate, the storagesystem is charged by the surplus energy generated. During peak demandperiods when electricity is consumed at higher than the average rate,the storage system is tapped to enable production of the neededadditional electricity while the main energy source, e.g. fossil boileror nuclear reactor, continues to operate at a constant rate.

Of the energy storage systems available in the prior art, pumped hydrois the most feasible. In the pumped hydro system surplus electricitygenerated during slack demand periods, is used to pump water to higherelevation, usually into a dammed lake, where it is retained. During highdemand periods, the water is released to flow down through hydroturbines, thereby generating needed electricity. Unfortunately, pumpedhydro energy storage is limited in application by a paucity ofacceptable sites for building dams and is further limited by oppositionfrom environment conscious groups opposing dam construction.

Another storage system available to steam cycle electric generatingplants is the removal of thermal energy directly from the steam cycleduring slack demand periods to be stored for later utilization highdemand periods. One such system known in the prior art diverts steamfrom the steam cycle to heat oil. Hydro carbons such as oil have heatstorage properties superior to those of water. However, oil typicallyloses its integrity if heated beyond 650 degrees Fahrenheit and islimited thereby. Steam temperatures in modern fossil fired plants canexceed 1,000° F. It is desirable to heat the energy storage medium tothe highest temperature possible to maximize heat recovery efficiency.The hot oil system is therefore inherently limited in that it cannot beused at the highest temperatures possible because of its loss ofintegrity. Moreover, no known liquid maintains its integrity at 1000° F.at moderate pressures. Solids, however, are superior heat storagemediums in that they maintain integrity at elevated temperatures and atlow pressure. Also, more heat per unit volume can be stored in solidsthan in liquids because of the greater density of the solidnotwithstanding a possible lower specific heat capacity.

One known system utilizing a solid for energy storage diverts hot fluidthrough holes in a solid block during slack demand periods therebycharging the block, ie., raising the temperature of the solid. Duringhigh demand periods, the block is used to heat cooler steam or waterthereby discharging the block, ie., returning the energy to the system.This system may be used at high temperatures, however, it has aninherent disadvantage. The temperature of the block during dischargethereof is not constant but rather is decreasing. As the temperature ofthe block decreases, the efficiency of heat transfer likewise decreases,resulting in a declining energy yield.

The present invention uses a bed of free-flowing refractory particlesfor heat transfer and heat storage and provides both a solid heatstorage medium for use at high temperature and a constant temperatureheat source during system discharge.

Apart from prior art in the field of heat storage technology, prior artexists in the field of free-flowing solid granules or microspheres as amechanism for heat storage and transfer for advanced energy source powerreactors. A typical description of research in this field is describedin the paper titled, "Moving Bed Heat Transfer for Advanced PowerReactor Applications" published by Mr. D. C. Schluderberg and Mr. T. A.Thornton at the Miami International Conference on Alternative EnergySources, in Miami Beach, Fla., Dec. 5 through 7, 1977. This paperreported the result of some tests conducted with gravity flow movingbeds of free-flowing microspheres over spiral tubing in a smalllaboratory-scale apparatus.

A number of proposals also were described in this paper forrecirculating articles from a hot reservoir through a steam generator toa cold reservoir for subsequent recirculation by means of an Archimedesspiral lift tube arrangement to the heat source and back to the hotparticle reservoir.

The concept of particulate material as a heat transport mechanism alsohas been the subject of intensive research. The following collection ofpatents, for instance, are illustrative of the work that has beenaccomplished in this field of technology. U.S. Pat. No. 2,672,671,granted Mar. 23, 1954, for alumina-mullite pebbles is directed to amethod of manufacturing high purity mullite-alumina pebbles that arecapable of enduring severe conditions of cyclic thermal and mechanicalshock. U.S. Pat. No. 2,644,799 granted July 7, 1953, for heat-exchangepebbles discloses the broad concept of a gravity-flow mass of pebblesfor discharging stored heat. The cooled pebbles after heat discharge,are recirculated by means of a bucket or screw conveyor. U.S. Pat. No.2,808,494, granted Oct. 1, 1957 for "Apparatus For Storing and ReleasingHeat" shows a gas or oil fired system for heating an immobilized mass ofpowder or spheres in an heat storage apparatus.

U.S. Pat. No. 2,856,506, granted Oct. 14, 1958 for "Method for Storingand Releasing Heat" is a division of U.S. Pat. No. 2,808,494 and largelyduplicates the disclosure in the '494 patent.

U.S. Pat. No. 3,615,187, granted Oct. 26, 1971 for "Process for theProduction of Spherical Alumina-Silica Containing Solid Particles Whichare Predominantly Mullite" is directed to production of the solidparticles rather than to some application techniques.

U.S. Pat. No. 3,669,889, granted June 13, 1972, for "Granular CeramicHeat Carrier Intended for Manufacture Thereof" describes a granularceramic heat carrier for use in conjunction with chemical processes. Themethod for manufacturing these granules also is described in thispatent.

In spite of the intensive research that has been applied to this generalarea of technology and clear energy conservation benefits of a practicaladaptation of these techniques notwithstanding, there is, nevertheless,a continued need to come forward with more efficient moving bed and heatexchanger combinations. Further in this respect, there is a requirementto adapt this technology to practical heating power plant generationcycles in order to make this technology immediately available to thepower utility industry.

These and other problems are satisfied to a large extent through thepractice of the present invention wherein an arrangement of one or moresilos are provided for absorbing heat from a mass of microspheres orother suitable particulate material. The microspheres absorb heat byflowing under gravitational force over heat exchanger tube bundles. Heatis provided illustratively from low and high-pressure heat water andreheat steam in a conventional power plant.

In the present invention, the plant steam turbine output is modulatedwhile fuel consumption remains constant. In typical steam cycle electricgenerating plants, portions of the cycle steam are at various pointsextracted for heating feedwater flow from the condenser to the steamgenerator in order to increase cycle efficiency. In the presentinvention, during off-peak periods, the steam generator remains at fullpower while turbine output is lowered by increasing extraction steamflow at various points in the steam cycle thus lowering flow rate to theturbines. The flow extracted above the normal amount is used to heat thestorage inventory of moving bed solids.

The extraction steam flows through a moving bed heat exchanger whilemoving bed materials flow down therethrough by gravity. In this way, bypermitting the particulate matter to absorb from different temperaturesteam supplies within the power plant system a much more efficient heatstorage and transfer system is provided. This system, moreover, isreadily adaptable to the reheat steam cycle that characterizes manymodern power generation plants today.

The hot moving bed solids are then stored in an insulated bin untilneeded. When peak demand power is required, the hot solids flow througha moving bed heat exchanger to heat feedwater flow directedtherethrough, thereby allowing a reduction of extracted steam flow belownormal. This reduction in extracted steam results in increased turbineoutput and increased electricity generation.

In this manner, heat storage is used to vary plant power output above orbelow an established baseload while power input from the plant heatsource is held constant at a level corresponding to the base loadelectrical output.

An object of the present invention is an energy storage and recoverysystem for storing excess energy generated by an electric power plantduring slack demand periods and for recovering the stored energy toprovide energy for producing supplemental electricity during peak demandperiods.

A further object of the invention is a system yielding for foregoingadvantages and which utilizes a moving bed of refractory particles for aheat transfer and storage medium.

Another object of the invention is a system yielding the foregoingadvantages and which can be back fitted to existing power plants.

A further object of the invention is a system yielding the foregoingadvantages and which can be used with fossil fueled plants or nuclearplants.

Other objects and advantages of the present invention will be readilyapparant from the following description and drawings which illustratethe preferred embodiments of the present invention.

SUMMARY OF THE INVENTION

The present invention involves a heat storage and recovery system forstoring excess over demand energy generated by a steam cycle electricalgenerating plant during slack electricity demand periods and forrecovering the stored energy to provide supplemental electricity duringpeak electricity demand periods.

The system utilizes one or more moving bed heat exchangers fortransferring heat between the steam cycle of the power plant and amoving bed of refractory particles. Pipes and valves establish fluidcommunication between the heat exchangers and the steam cycle to supplyfluid to selectively heat the moving bed of refractory particles or tocool them as the case may be.

One or more insulated silos are provided for storing the refractoryparticles and means are provided for transporting the particles betweenthe silos and the heat exchangers.

BRIEF DESCRIPTION OF THE DRAWINGS

FIG. 1 is a schematic diagram of a fossil fired electric powergenerating plant steam cycle utilizing an energy storage systemaccording to the present invention.

FIG. 2 is a graph showing the temperature of the moving bed refractoryparticles through the moving bed heat exchanger of FIG. 1 as a functionof percent heat transferred.

FIG. 3 is a partial cutaway elevation view of a preferred embodiment ofmoving bed heat transfer and storage equipment of a system according tothe present invention.

FIG. 4 is a view like FIG. 3 of a heat exchanger of FIG. 3.

FIG. 5 is a view taken along line V--V of FIG. 4.

FIG. 6 is a schematic diagram like FIG. 1 showing an alternateembodiment of the invention.

FIG. 7 is an elevation view of a two silo system according to thepresent invention.

FIG. 8 is a view like FIG. 7 of a 3 silo system.

FIG. 9 is a view like FIG. 8 showing a one silo one heat exchangerarrangement.

FIG. 10 is a view like FIG. 1 of a nuclear power plant steam cycle.

FIG. 11 is a partial elevation view of tube banks according to thepresent invention.

FIG. 12 is a partial bottom view taken along line XII--XII of FIG. 11.

DETAILED DESCRIPTION

Refer now to FIG. 1, there being shown schematically an energy storagesystem according to the invention incorporated into a fossil firedelectricity generating plant steam cycle. The steam cycle shown in FIG.1 is a simplified version showing only necessary component parts.Typically, such systems incorporate more intricate steam bleed andfeedwater heating features and other efficiency related features notpertinent to the invention and therefore not shown in the figure.

The fossil fired steam cycle of FIG. 1 is isolated from the heat storagesystem by valves 104, 108, 110 and 112. In the steam cycle, systemwater, or steam as the case may be, is heated by hot combustion gases infour sections: economizer 52, boiler 54, superheater 62, and reheater68. Subcooled water in line 51 flows through economizer 52, wherein thewater is heated to near boiling temperature. The water then flowsthrough boiler 54 wherein it is raised to boiling temperature andconverted to steam. Line 51 empties into the steam drum 56 wherein anyunboiled water precipitates to the bottom thereof and flows through line59 and into line 51 to be recirculated through boiler 54. Steam, fromsteam drum 56, flows through superheater 62 via line 61 wherein thetemperature of the steam is raised above the boiling temperature, ie.,superheated.

The steam continues through line 61 to expand through and turn highpressure turbine 64. The steam exits turbine 64 via line 67, is reheatedin reheater 68, and enters intermediate pressure turbine 70. The steamexpands through intermediate pressure turbine 70 and exits via line 73to enter low pressure turbine 74. The steam again expands in lowpressure turbine 74 and exits via line 77.

Turbines 64, 70, and 74 and electrical generator 80 are mounted on acommon shaft 78.

The steam then enters condenser 82 and therein heats condensing fluid inline 85 and condenses to water.

The heat gained by the condensing fluid in line 85 is eventuallydissipated to the environment, e.g., by discharging into a body of wateror by evaporation into the air via a cooling tower (not shown).

The water in line 87 is then pumped up to feedwater pressure by pump 88and enters feedwater line 51. Steam is extracted from intermediatepressure turbine 70 via line 91 and from low pressure turbine 74 vialine 93 and 95 for heating feedwater in line 51. Steam in lines 91, 93and 95 flow through feedwater heaters 96, 98 and 100, respectively,being condensed therein collected in line 103 and fed into line 51. Thepurpose of feedwater heating is to increase cycle efficiency. The waterin line 51 now flows back to econimizer 52, completing the cycleefficiency.

The above described portion of FIG. 1 pertains to a fossil fired steamcycle without energy storage capacity. The below described energystorage system according to the invention is added to the abovedescribed cycle to increase peak generating capability.

The primary component of the energy storage system, silo, generallydesignated by reference numeral 10, is shown schematically in the systemdiagram of FIG. 1 and in more detail in FIG. 3.

Referring to the schematic diagram, FIG. 1, the silo 10 includescharging heat exchanger, storage bin 16, and discharging heat exchanger18.

Free-flowing refractory particles are utilized as a heat storage medium.These particles should be spherical in shape, have a uniform size ofabout 100 microns and be inexpensive. Acceptable materials includesilica sand, barytes sand (barium sulfate), partially calcined clay,glass beads and reclaimed petroluem catalysts. In the embodiment of theinvention described herein, silica sand is used as the heat storagemedium.

During slack electrical demand period, sand 13 is poured down throughthe exchanger 14 being heated therein. Heated sand 13 falls from heatexchanger 14 to bin 16 to be retained therein.

Heat exchanger 14 is divided into sections 14a, 14b, 14c, 14d, 14e and14f. During slack electricity demand periods, steam is diverted from thecycle and routed through heat exchanger 14. The resulting decreases inthe flow rate of the steam entering the turbines reduces turbine shaft78 and generator 80 speed and thereby reduces electricity generated bygenerator 80. With valve 104 open, superheated steam is extracted fromline 51 and routed to steam generator section 14a via line 105. Line 105exits section 14a and continues in turn through section 14c, 14d and14f. The steam is reduced to saturation temperature in sections 14a and14c condensed in section 14d and cooled to feedwater temperature insection 14f. Subcooled water in line 105 is pumped back to feedwaterline 51, via line 107 by pump 116.

With valve 108 open, additional steam is extracted from line 67downstream of reheater 68 and routed via line 109 through heat exchangersection 14b and section 14e being cooled therein to pre-reheattemperature and returned to line 67 upstream of reheater 68 by pump 114.

Refer now to FIG. 2 showing typical temperature curves for heatexchangers 14 and 18 as a function of percent heat transferred to andfrom sand 13 respectively. Curve 13' represents the temperature of sand13 as a function of percent heat transferred. As sand 13 enters heatexchanger 14 at about 270° F., no heat has yet been transferred. As sand13 leaves heat exchanger 14 at approximately 800° F., sand 13 will gainno more heat therefore percent heat transferred equals 100 percent.Curve 13' would be a straight line function if the specific heatcapacity of sand 13 was constant. However, heat capacity is not constantbut rather a function of temperature and therefore curve 13' is slightlycurved.

Curves 14'a, 14'c, 14'd, and 14'f represent the steam/water temperaturein line 105 of FIG. 1 as it passes through heat exchanger sections 14a,14c, 14d and 14f respectively. Curve 14'b and 14'e represent the steamtemperature of line 109 as it passes through heat exchangers 14b and 14erespectively.

Refer back to FIG. 1. During peak demand periods, heated sand 13 isreleased from bin 16 through heat exchanger 18 being cooled therein.Heat exchanger 18 is divided into two sections, 18a and 18b. Openingvalve 110 allows feedwater from line 51 upstream of reheaters 96, 98 and100 to enter line 111 and pass through section 18b being heated thereinto downstream reheater temperature. Opened valve 112 allows feedwaterdownstream of feedwater heaters 96, 98, and 100 to enter line 113 beingjoined by line 111 to pass through section 18a and rejoin main feedwaterline 51 downstream of economiser 52.

Refer now to FIG. 2. Curves 18'b and 18'a represent the watertemperature in lines 111 and 113 respectively through heat exchangers18b and 18a respectively. FIG. 2 illustrates the judicial selection ofpoints in the steam cycle from which steam is extracted, and theselective routing to heat exchanger sections to maintain adequatetemperature differences between steam and sand 13 in the heatexchangers.

Further, extraction flowrates and sand flowrates are chosen such thatsteam or water, as the case may be reenters the steam cycle at thetemperature of the steam cycle fluid at the reentry point.

With charging heat exchanger 14 operating at the temperatures of FIG. 2,the mass flowrate in line 105 is about 180,000 pounds per hour, the massflowrate in line 109 is about 150,000 pounds per hour, and the massflowrate of sand is about 1.7 million pounds per hour.

With discharging heat exchanger 18 operating at the temperatures of FIG.2, the mass flowrate of water through line 111 is about 150,000 poundsper hour and about 670,000 pounds per hour through the line 113 with asand mass flowrate of about 1.0 million pounds per hour.

With a charging mass flowrate of 1.7 million pounds per hour and adischarging mass flowrate of 1.0 million pounds per hour, the period ofdischarge is obviously longer than the period of charge. The system maybe designed to accommodate a particular power plant's peaking cycle.Baffles (not shown) of heat exchangers 14 and 18 limit sand 13 flowrate.

During peak electricity demand periods, operation of heat exchanger 18as above described increase the enthalpy of feedwater entering theboiler above normal enthalpy levels resulting in the production of steamin the boiler at a faster rate and a lower fraction of water beingreturned to the boiler via line 59. The increased steam flow rate turnsthe turbines faster and thereby increases generator electrical output tosatisfy peak electricity demands.

Refer now to FIG. 3, there being shown silo 10 in accordance with apreferred embodiment of the invention. Storage bin 16 of silo 10includes a hollow cylindrical barrel 30 topped by inverted funnel shapedupper cover 32 and enclosed on the bottom by funnel shaped lower cover34. Upper cover 32 is open at the top. Heat exchanger 14 is positionedabove storage bin 16 and connected thereto via duct 15. Conical baffles36 and 38 are disposed interior to lower cover 34 and are open at thetop and the bottom. Baffles 36 and 38 are supported by horizontalsupport grid 40. Any suitable support structure that will not obstructthe sand flow may be used in grid 40. Baffles 36 and 38 ensure that sandempties into heat exchanger 18 uniformly. In the absence of baffles 36and 38, sand 13 in the center of bin 16 would sink faster than sand 13near the walls of bin 16. Bin 16 communicates with heat exchanger 18 viaconnecting conduit 17.

Conveyor 28 is positioned to receive sand 13 flowing out of heatexchanger 18 and to deposit sand 13 into receiver 24 of bucket elevator20. Bucket elevator 20 extends up above the top of silo 16 and emptiesthrough spout 22 to conveyor 26 positioned thereunder. Conveyor 26extends from spout 22 to above heat exchanger 12. Diverters 27 divertsand from conveyor 26 into hopper 29.

Silo 10 according to the invention operates in either a charging mode ora discharging mode. In operation of the charging mode, bin 16 isinitially filled with cold sand 13. To heat sand 13, steam extractedfrom the steam cycle of an electric generating plant during a slackelectric demand period is diverted through heat exchanger 14. Plate 33is withdrawn allowing sand to flow through perforated plate 31, out ofsilo 16 and onto to conveyor 28. Sand 13 is carried by conveyor 28 andfalls off into receiver 24. Bucket elevator 20 lifts sand 13 to the topthereof to be poured out spout 22 and deposited on conveyor 26. Bucketelevators are commercially available being capable of operating underthe desired conditions. One such bucket elevator is available as modelF10 from Universal Industries, 1575 Big Rock Road West. Waterloo, Iowa50701. Sand 13 is then conveyed over heat exchanger 14 by conveyer 26deposited therein. Diverter 27 is angled to divert sand 13 from conveyor26 and into hopper 13. Sand 13 flows down through heat exchanger 14being heated therein and through neck 15 and into bin 16.

A static, subtle bed of the refractory particles has a sufficiently lowthermal conductivity, such that it is possible to store separatequantities of hot and cold bed material in the silo 16 withoutsignificant heat transfer between them. Silo 16 can therefore remainfull while containing varying amounts of hot and cold material dependingon point in time for the heat storage cycle. For this reason, storagevolume tends to be 50 percent less than for systems using heat transferfluids stored in separate hot or cold tanks.

Turning now to FIGS. 4 and 5, a typical steam generator arrangement forheat exchanger 14 is shown. Inlet header 42 establishes fluidcommunication with the tubes in tube bank 41. The tubes in this bank arearranged in vertical segments, each of the ends of the segments beingsupported by perforated baffle plates 48. Steam generated within tubebank 41 is discharged from the heat exchanger 14 by way of acommunicating steam outlet header 44. Immediately below the heatexchanger 21 the discharge shutter or orifice plate 33 (FIG. 3) ispositioned to control the density of the bed of flowing paticles 13which are flowing over the tubes in the tube bank 41. The individualtubes in the tube bank 41 are arranged in a generally horizontalorientation in a staggered array that is designed to promote a highdegree of flow mixing with the particles 13. In these conditions heattransfer coefficients are expected to exceed those achieved in afluidized bed (which bed would have the same particles in surroundinggas) by a factor of 5 or more. Such results appear quite reasonable whenit is remembered that particle concentrations and velocities on the heattransfer surface in a fluidized bed are much lower. Furthermore, contactwith streams of the most dense mixtures (which flow downward around therising bubble) is intermittent and somewhat uncontrollable at any givenlocation. Turning once more to the illustrative steam generator 14 shownin FIGS. 4 and 5, for the purpose of this specific embodiment of theinvention, diaphragms are used in the vertical headers to produce thedesired size, tube side flow pass in each heating or cooling section,and also to separate heating sections operating at different steampressures. The horizontal tube banks consist of 0.75-inch outsidediameter tubes on 0.85-inch triangular pitch with 17 tubes per row (seeFIG. 11). Tube ends are swaged to 0.625 inch outside diameter to provideadequate tube sheet ligament. Casing walls for the heat exchangers arehorizontally corrugated in order to prevent the particles 13 frompassing along the casing walls. Tube rows, moreover, are spaced by useof 0.10 inch thick rings (not shown) spaced at suitable intervals alongeach tube, extra vertical spacing between tubes at header diaphragmlocations are fitted with perforated orifice plates 48 (FIG. 12) tomaintain the even particle flow velocity over the tube bank above andassure a high bed density in contact with the entire tube periphery.Orifice plates in turn rest upon support steel to carry the verticalload and tube weight in each bank.

Existing plants appear suitable for tolerating suitable increases inextraction steam flow and to decrease in turbine throttle flow for thecharge mode of the moving bed thermal storage cycle described above.However, a peaking steam generator and turbine generator are required,to provide the on-peak desired power, unless the plantsturbine-generators have excess superheat capability beyond base load.

Refer now to FIG. 6 wherein another embodiment of the present inventionis shown. FIG. 6 illustrates the same steam cycle of FIG. 1 wherein apeaking steam cycle is provided because the existing turbine generatorsare not capable of stretched operation. Steam is generated in dishcargeheat exchanger 21, flows via line 131 to turbine 132 to expandtherethrough. The cycle continues through condenser 135 and pump 136 andback to heat exchanger 21 to complete the cycle. Peaking generator 138is driven by turbine 132 via shaft 134.

Also shown in FIG. 6 is the use of extraction steam from lines 91, 93and 95 in charging heat exchanger sections 19c, 19b and 19a,respectively. Reheat steam is utilized in section 19d as above describedfor FIG. 1.

Refer now to FIG. 7 which shows a two-silo system which avoids the needfor internal distribution baffles and allows greater latitude in siloproportions aimed at achieving lower capital costs. It also providesgreater adaptability to variatons in system peak-load characteristics.Thus, as shown in FIG. 7, two silos are provided, a hot silo 71, and acold-surge silo 72. Hot silo 71, is continuously serviced by operatingthe fossil-fired heat source to supplement the daily off-peak availableenergy. This heat is applied to the particulate matter within the siloby way of a continuous charge heat exchanger 122, in whichillustratively, hot gas or air provides the heat source. Heat exchanger122 is mounted in the heat charging section of silo 71, immediatelybelow the conveyor belt 128. Hot silo 71 has immediately below thecontinuous charge heat exchanger, a heat storage section 120, which inturn is immediately above the discharge heat exchanger 124, thus,discharge heat exchanger 124 extracting heat from the flowing particlesproduces steam of a suitable quality. The now cool particles flow fromsilo 71 onto a discharge conveyor 126 for transportation to aconventional bucket elevator 150 for recycle through the system viaconveyers 146 and 128 and bucket elevator 130 in the manner previouslydescribed in connection with FIG. 3.

Particles stored in cold-surge silo 72 vary plant output above or belowan established base load, while power input from the plant heat sourceis held constant at a level corresponding to the base load while powerinput from the plant heat source is held constant at a levelcorresponding to the baseload requirements. The objective of thesesystems is to provide intermediate, on-peak load power at combined fueland capital cost which is favorable when compared with competing methodssuch as oil-fired gas turbines, pumped hydro, combined cycles oradditional system tie-in.

Pressurized water nuclear power reactor applications can utilize atriple silo arrangement to permit the combined use of off-peak nuclearheat together with continuous input from suitable coal-fired equipment.

The boiling water reactor also could use a triple silo arrangement butwould also require a reboil that would produce uncontaminated, that is,dry steam if off-peak nuclear heat for it to be stored. Liquid metalfast breeder reactors and high temperature gas cooled reactors have avariety of options, facilitated by higher operating temperatures and lowfuel costs wherein a two or three silo arrangement would be used to meetvarying amounts of intermediate on-peak load with or without additionalfossil heat.

Further efficiencies in nuclear power systems can be maximized bysupplementing the nuclear heat with fossil fuel produced heat to producehigher bed temperatures.

FIG. 8, for example, shows a heat storage system operating on the basisof a 30 percent nuclear heat and 70 percent coal combination. Heat lossper day was assumed to be 7.5 percent. The silo system shows first silo162 in which the charging heat exchanger equipment receives its heatfrom input off-peak nuclear energy. This silo stores particles at 505degrees Farenheit and discharges these particles into heat exchanger 164which is serviced continuously by heat from the coal-fired source ofsteam. These heated particles then flow through silo 166, whenappropriate, to be discharged over heat exchanger 168 in order toproduce steam at appropriate conditions. The discharged particulatematerial then is conveyed in the direction shown by line 84 to the inletof a third silo 170 where the particles are stored at 275 degreesFarenheit. Note in this respect that the particles were stored at atemperature of 1,025 degrees Farenheit in silo 166.

Discharged particles from silo 170 then flow in the direction indicatedby means of line 86 back to silo 162, first flowing over the off-peaknuclear energy supplied heat in the heat exchanger 160 at the inlet tothe silo 162. This silo system was designed to provide 18 megawattselectric power output for 11.5 hours which complies with a 200 megawattelectric plant base load output. Overall plant thermal efficiency wastaken as 33 percent. In operation, during off-peak periods the entireinventory of silo 170 flows through the nuclear steam heated section inheat exchanger 160 to enter the silo 162.

However, during this time, there is a continuous flow of particles outof silo 162 and into silo 166. During the 14-hour discharge period,particles will flow from silo 166 into silo 170. In this way, athree-silo system stores off-peak reactor thermal energy and supplementsit with continuously supplied energy from coal or some other fossilfuel. Thus, there is provided in accordance with the invention, animproved system for storing heat during off-peak load conditions andutilizing this stored heat to supplement plant steam generating capacityat peak load conditions.

Refer now to FIG. 9 showing an alternate embodiment of the presentinvention. A single moving bed heat exchanger 200 is used in thisembodiment to both heat and cool the sand. A pair of Archemedes lifts210 and 212 transport the sand between heat exchanger 200 and silo 10.

Fluid to be cooled or heated flows through tube bank 201. Moving bedmaterial flows down through heat exchanger 200 around tube bank 201 tobe charged by extracted steam or to be discharged by heating feedwaterflow in the manner described above. In this embodiment adequate pipingand valves (not shown) are provided to supply either extracted steam orfeedwater to the steam cycle side of moving bed heat exchanger 200 foreither charging or discharging respectively.

In the embodiment of FIG. 9 bin 16 is supported by earth 215. Thismanner of support allows for more economical bin structure and providesinsulation for minimizing heat loss from bin 16.

Archemedes lifts are well known in the art and comprise an inclinedthreaded screw 214 encased by a cylinder 216. As screw 214 and casing216 turn together, material laying on the bottom edge of the screw istransported upward along the screw threads.

In FIG. 9, sand is transported by Archemedes lifts 212 and 210 in thismanner. To minimize effort required to turn the lifts 210 and 212 theindividual pockets of sand laying therein are fluidized, thus,decreasing the friction between the sand and the lifts. Illustratively,this can be accomplished by maintaining a pressure differential betweenend 220 and end 221 of lift 210. The resulting air forced through lift210 bubbles through pockets of sand 219 to fluidize them. By sealingends 220 and 221 air 218 pumped by lifts 210 itself is forced backthrough sand pockets 219 to fluidize them. Alternatively, a blower (notshown) may be provided to pump air through lift 210.

Refer now to FIG. 10 showing the single heat exchanger 200 utilized in anuclear power plant steam cycle. In the charging mode valves 230, 232,233 and 235 are closed and valves 231, 234 and 236 are open. Highpressure steam from steam generator 237 enters the top of heat exchanger200 passes therethrough to heat sand 13 and reenters steam generator237.

Additional high pressure steam having been compressed by compressor 238enters heat exchanger 200 from the bottom exits through water turbine239 and flows back to steam generator 237.

In the discharging mode, valves 231, 234 and 236 are closed and valves230, 232, 233 and 235 are open. Feedwater enters heat exchanger 200 atthe bottom, is joined by heated feedwater admitted through valve 232 andexits to enter the steam generator at an elevated enthalpy level.

The above description and drawings are only illustrative of severalembodiments which achieve the objects, features and advantages of thepresent invention, and it is not intended that the present invention belimited thereto. Any modifications of the present invention which comewithin the spirit and scope of the following claims are considered partof the present invention.

What is claimed as new and desired to be secured by Letters Patent ofthe United States is:
 1. A heat storage and recovery system for storingexcess over demand energy generated by a steam cycle electricalgenerating plant during slack electricity demand periods and forrecovering the stored energy to provide supplemental electricity duringpeak electricity demand periods comprising:moving bed heat exchangermeans for exchanging heat between said system and the generating plantwherein said moving bed exchanger means comprises: an inlet headerhaving an inlet tube sheet; an outlet header having an outlet tubesheet; said inlet header having at least one inlet for admitting fluidto said heat exchanger; said outlet header having at least one outletfor discharging fluid from said heat exchanger; a plurality of tubebanks each extending generally horizontally from said inlet tube sheetto said outlet tube sheet to establish fluid communication therethroughbetween said inlet header and said outlet header; a shell encasing saidplurality of tubes and being open at the top and the bottom; said inletheader and said outlet header each having a plurality of diaphragmsdividing said headers into a plurality of compartments; said pluralityof diaphragms including a number of section diaphragms being positionedin said headers between a corresponding number of same pairs of tubebanks to divide the heat exchanger into a corresponding number ofsections, and further including a number of subsection diaphragms beingpositioned in said headers between every other pair of tube banks andstaggered as between headers such that each of said compartments is influid communication with the inlet and the outlet of its section; saidtube banks having a plurality of tubes being on a triangular pitchedarray and a plurality of orifaced plates extending below each of saidtube banks to support said tube banks and to retard the flow of sandtherethrough over said tubes to provide an even sand flow velocitythrough the shell side of said heat exchanger and to provide a high sandbed density in contact with the entire periphery of each tube;conduitmeans for establishing fluid communication between the steam cycle andsaid moving bed heat exchanger means wherein said conduit meanscomprises: a plurality of turbine steam extraction pipes to separatelydivert intermediate and low pressure turbine steam to said heatexchanger means; a plurality of feedwater heat pipes to separatelydirect the fluid diverted by said plurality of turbine steam extractionpipes, after having passed through said moving bed heat exchanger means,through feedwater heaters to be returned to the steam cycle at the mainfeedwater portion of the cycle; a third pipe to establish fluidcommunication between the reheat portion of the steam cycle and saidmoving bed heat exchanger means for extracting reheated steam from thesteam cycle; a fourth pipe to establish fluid communication between saidmoving bed heat exchanger means and the steam cycle below the highpressure turbine and above the reheater to return the fluid extractedfrom the steam cycle via said third pipe; and, a fourth pipe pump topump the fluid through said pipe; valve means for selectively openingand closing said conduit means to selectively admit fluid from differentpoints in the steam cycle to said moving bed heat exchanger means; a bedof refractory particles of suitable size for flowing through said movingbed heat exchanger means; storage means for storing said bed ofrefractory particles; and, transport means for transporting saidrefractory particles between said storage means and said moving bed heatexchanger means.
 2. A system as in claim 1 further comprising a recoverymode steam cycle for producing electricity during peak electricitydemand periods, including,a recovery turbine-generator, a recoverycondenser, a recovery pump, andrecovery conduit means for directingfluid through said moving bed heat exchanger means, through saidrecovery turbine generator, through said recovery condenser, and throughsaid recovery pump and back to said moving bed heat exchanger means tocomplete the cycle.
 3. A system as in claim 1 wherein: said storagemeans includes a hot silo and a cold silo;said moving bed heat exchangermeans includes a charging heat exchanger positioned above said hot silowherein said refractory particles are heated by steam directed from thesteam cycle, and a discharge heat exchanger positioned below said hotsilo wherein feedwater is heated by said refractory particles; and, saidtransport means includes a first bucket elevator for lifting sand frombelow said discharge heat exchanger to above said cold silo, a secondbucket elevator for lifting sand from said cold silo to above saidcharging heat exchanger, first conveyer means to convey said refractoryparticles flowing out of said discharge moving bed heat exchanger tosaid first bucket elevator, second conveyer means to convey saidrefractory particles from said first bucket elevator to said cold silo,third conveyer means to convey refractory particles flowing from saidcold silo to said second bucket elevator, fourth conveyer means toconvey sand from said second bucket elevator to said charging heatexchanger to flow down therethrough.
 4. A system as in claim 1 wherein:said storage means includes a single insulated silo;said moving bed heatexchanger means includes a single moving bed heat exchanger for bothcharging and discharging said bed of refractory materials; saidtransport means includes a first Archimedes' lift to move saidrefractory particles from below said silo to above said moving bed heatexchanger and a second Archimedes' lift to move said refractoryparticles below said heat exchanger to above said silo.
 5. A system asin claim 4 where each of said Archimedes' lifts include a pressurizingmeans to maintain a pressure differential between the ends of each ofsaid lifts to promote the diffusion of air through the lift therebyfluidizing the refractory particles being conveyed therein.
 6. A movingbed heat exchanger comprising:an inlet header having an inlet tubesheet; an outlet header having an outlet tube sheet; said inlet headerhaving at least one inlet for admitting fluid to said heat exchanger;said outlet header having at least one outlet for discharging fluid fromsaid heat exchanger; a plurality of tube banks each extending generallyhorizontally from said inlet tube sheet to said outlet tube sheet toestablish fluid communication therethrough between said inlet header andsaid outlet header; a shell encasing said plurality of tubes and beingopen at the top and the bottom; said inlet header and said outlet headereach having a plurality of diaphragms dividing said headers into aplurality of compartments; said plurality of diaphragms including anumber of section diaphragms being positioned in said headers between acorresponding number of same pairs of tube banks to divide the heatexchanger into a corresponding number of sections, and further includinga number of subsection diaphragms being positioned in said headersbetween every other pair of tube banks and staggered as between headerssuch that each of said compartments is in fluid communication with theinlet and the outlet of its section; said tube banks having a pluralityof tubes being on a triangular pitched array; and a plurality oforifaced plates extending below each of said tube banks to support saidtube banks and to retard the flow of sand therethrough over said tubesto provide an even sand flow velocity through the shell side of saidheat exchanger and to provide a high sand bed density in contact withthe entire periphery of each tube.